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纳米铁基催化剂在CO2加氢制烃中的性能 被引量:5

Properties of the Nano-Particle Fe-Based Catalyst for the Hydrogenation of Carbon Dioxide to Hydrocarbons
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摘要 使用尿素沉淀凝胶、机械混合和等体积浸渍相结合的方法, 制备了一系列的纳米尺寸FeK-M/γ-Al2O3(M=Cd,Cu)催化剂, 采用扫描电镜(SEM)、透射电镜(TEM)、N2物理吸附、X射线衍射(XRD)光谱和H2程序升温还原(H2-TPR)仪对催化剂进行表征, 并在小型固定床反应器上考察其对 CO2加氢反应的催化性能. 结果表明:3 MPa, 400℃, 3600 h-1, H2/CO2摩尔比为3的条件下, 15%(w, 下同)Fe10%K/γ-Al2O3催化剂可稳定运行100h 以上, CO2转化率为51.3%, C2+烃类的选择性达62.6%. Fe含量降至2.5%时, C2+烃类的选择性仍能达到60.0%. 随着 K 含量由 0%增加至 10%, 低碳烯烃选择性增加, 烯烷比增加至 3.6. Cd 和 Cu 助剂可促进 Fe 物种的还原, 改善目的产物的分布, 其中Cu的加入使低碳产物烯烷比增至5.4, Cd的加入使C5+产物选择性增加了12%. Combining co-precipitation-gelation, mechanical mixing and impregnation methods, a series of catalysts of FeK-M/γ-Al2O3(M=Cd or Cu) have been attained. The catalysts were characterized by scanning electron microscopy (SEM), transmission electron microscopy (TEM), N2 physisorption, X-ray diffraction (XRD) and temperature-programmed reduction of hydrogen (H2-TPR). The hydrogenation of carbon dioxide over these catalysts was also investigated in a fixed bed. Given a reaction time of 100 h, CO2 conversion over a 15%Fe/10%K/γ-Al2O3 catalyst reached 51.3 %, with a selectivity towards C2+ of 62.6 % at 3 MPa, 673 K, a space velocity of 3600 h-1 and at a molar ratio of H2/CO2 of 3. At the lower Fe content of 2.5%, the selectivity towards C2+ was still greater than 60.0%. Increasing the potassium content from 0% to 10%, increased the selectivity towards C2-C4= and the molar ratio of C2-C4= /C2-C40 increased to 3.6. The addition of Cd and Cu improved the reduction and catalytic activities. Specifically, Cu improved the molar ratio of C2-C4= /C2-C40 from 3.6 to 5.4, and the Cd increased the selectivity of C5+ by 12%.
出处 《物理化学学报》 SCIE CAS CSCD 北大核心 2012年第8期1943-1950,共8页 Acta Physico-Chimica Sinica
关键词 二氧化碳:加氢转化:铁基催化剂:沉淀:低碳烃类 Carbon dioxide Hydrogenation Fe-based catalyst Precipitation Light hydrocarbon
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  • 1阎世润,周敬来,林恒生.助剂对FT合成Fe—Mn共沉淀催化剂的影响 Ⅱ 催化剂的XPS研究[J].天然气化工—C1化学与化工,1993,18(6):8-13. 被引量:1
  • 2吴宝山,白亮,张志新,相宏伟,李永旺,易凡,徐斌富.不同沉淀剂制备的铁基催化剂对浆态床F-T合成反应的催化性能[J].催化学报,2005,26(5):371-376. 被引量:15
  • 3赵玉龙,王佐.Sasol的浆态床FT合成技术[J].煤炭转化,1996,19(2):54-58. 被引量:8
  • 4GEERLINGS J,WILSON J,KRAMER G.FischerTropsch technology-from active site to commercial process[J].Applied Catalysis A:General,1999,186:27-40.
  • 5KRYLOVA A LAPIDUS A,TSAPKINA M V.Process for the preparation of high activity carbon monoxide hydrogenation catalysts;the catalyst composition,use of the catalysts for conducting such reactions,and the products of such reactions:US,6313062[P].2001-11-6.
  • 6ARCURI K,AGEE K,AGEE M.Structured Fischer Tropsch catalyst system and method:US,6797243[P].2004-9-28.
  • 7OREAR D.Conversion of syngas to distillate fuels:US,6864398[P].2005-3-8.
  • 8JOEP J,FREIDEA F,GAMLIN T.An adventure in catalysis:The story of the BP F-T catalyst from laboratory to full-scale demonstration in Alaska[J].Topics in Catalysis,2003,26(1-4):3-12.
  • 9DRY M.Practical and theoretical aspects of the catalytic Fischer-Tropsch process[J].Applied Catalysis A:General,1996,138:319-344.
  • 10ADESTINA A.Hydrocarbon synthesis via Fischer Tropsch reaction:Travails and triumphs[J].Applied Catalysis A:General,1996,138:345-367.

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